Continuous disk filter



- Aug 205 34M J. T. DlcKlNsoN ET AL 2,@

CONTINUOUS DISK FILTER Filed Jan. 3l, 1942 5 Sheets-Sheet l Aug 20 3946 J. T. DlcKlNsoN l-:T AL

l .I CONTINUOUS DISK FILTER Filed Jan. 31, 1942 5 Sheets-Shed', 2

` Aug 20, 1946. .1. AT. DlcKlNsoN 'E1-AL 2,496,065

CONTINUOUS DISK FILTER Aug 20, i946.. JIT. DlcKlNsoN ET AL CONTINUOUS DISK FILTER Filed Jan. 31, 1942 5 sheets-sheet 4 v mm MR Tw Em NF OK sm ND JKJS mm Dm Tw C Aug. 20, 1946.

lFiled Jan. 3l, 1942 5 Sheets-Sheet 5 Patented Aug. 20, 1946 CONTINUOUS DISK FILTER John T. Dickinson, Baskiug- Ridge, and Arthur R. Moerman, Alpine, N. J., assignors to Standard go, Ill., a corporation of Oil Company, Chica Indiana Application January 3]., 1942, Serial No. 429,044

This invention relates to a continuous disk iil- "5l ter and it pertains more particularly to improvements in a continuous disk filter for adapting it to special uses. The invention is directed primarily to filter structure for use in the dewaxing of mineral oils but the invention is not limited@ to such use.

An object of our invention is to provide an improved disk iilter assembly which can easily be fabricated, adjusted, repaired and operated,

an assembly whichavoids the numerous disad- 12 claims. (c1. zio-' zoo) proved correlation of structural elements and controls whereby' the iilter may` be assembled and operated at minimum expense and with maximum eiectiveness.

A further object of our invention is to provide a compact iilter with maximum filter area and to markedly increase the filter rates obtainable. A further object is to minimize the holding time in the iilter of a slurry which is undergoing filtration and to prevent undue settling out of solids from such slurry.

A further object is to provide a new and improved structure for filter disc sectors, means for securing lter elements to said sectors and means for keeping said iilter elements out of direct contact with a-scraper or cake deiiector. A

. further object is to provide an improved method and means for washing and drying a filter cake on disk filter sectors and for back Washing and cleaning the lter elements on said sectors.

A further object is to provide a new and improved cake discharge system including means for correctly and automatically positioning the scraper blade or deflector with respect to all parts of the filter disk sector and means for automatically compensating for any slight radial sector disalignment. A further object is to provide means for simultaneously regulating the position of all scraper blades in the filter assembly.

A further object is to provide improved'methods and means for inspecting the operation of a closed pressure iilter and for regulating the operation thereof from a point outside of the filter.

A further object is to provide improved method and means for avoiding iilter slurry contamif 2 nation by wash liquid running down the tie rods.

A further object is to provide an improved lter structure for effecting the separation of waxv from a cold propane oil solution whereby more rapid iilter rates, higher dewaxed oil yields, better wax cakes and lower pour point differentials are obtainable than have heretofore been possible. Other objects will be apparent as the detailed description of our invention proceeds.

Briefly, our invention comprises a unitary pressure vessel containing a horizontal rotatably mounted shaft which supports a plurality of flter disks. Individual slurry pans are provided in the lower part of the chamber for each filter disk, the pans being only slightly wider than the thickness of the iilter disk, being interconnected by conduits for uniform operation and being securely welded to the iilter structure. A single liquid level control device automatically maintains a slurry level in each and all of these pans. Wax discharge hoppers are mountedbetween adjacent pans on one side of the assembly and these hoppers direct the wax cake to a; screw conveyor which removes the wax cake from the filter. An important featureY of our invention is the floating deflector blades which may be adjusted upwards, sidewards and laterally, which are held under substantially uniformtension and which automatically follow the contour of the filter sectors regardless o-f any slight misalign-n ments. The position of all of these scraper blades may be changed by a single externally operated control.

Cake washing and iilter cleaning liquids may be sprayed against the viilter elements in their upper position and an outstanding feature of our invention is the method and means for preventing such liquids from contaminating the liquid slurry. Any liquids which run down the tie rods are caught in specially designed cups and are thus deflected into a catch pan which may lead to the cake discharge hoppers or to a separate draw-off line.

Individual sectors have convex instead of flat surfaces and the iilter element is held against the convex surfaces by a continuous wire wrapping. By employing continuous wire wrapping instead of welding the wire at each edge of the sector we avoid untold breakage diculties. The convex shape of the sector cooperates with the wire wrapping for holding the lter element in to the pores of the lilter element and protects the filter element against unduewear.

Each face of the filter sector is provided with parallel and relatively shallow channels Which are closed at one end and which communicate with a filtrate removal trough at the other. As the sector moves upwardly the filtrate flow is downward through the channels to the trough so that the channels are rapidly emptied but as the sector moves downwardly on the other side of the filter the closed end of these channels acts as a dam and each of the channels remains full of liquid. In the blow-back Voperation-this liquid is forced uniformly through the entire filter element for discharging wax cake therefrom and for effectively cleaning the filter element for reuse.

Each sector of a given lter disk communicates with a separate horizontal duct in the rotating shaft and this duct in turn communicates with the master valve leading to the ltrate port, the wash-liquid port and the blow-back port refilter casing which are kept clear by individual propane sprays or sprays of other liquids.

The invention will be more clearly understood from the detailed description of a preferred'embodiment thereof read in conjunction with the accompanying drawings which form a part of this with a removable head but which is preferably provided with a removable manhole cover II for permitting access to the interior thereof. The pressure vessel I9 may be mounted on suitable lugs I2 resting upon a concrete foundation or steel support. I n each end of the vessel lugs I2 (Figures 2 and 3) are welded, preferably above cerspecification. in which similar parts are desig-f A nated by like reference characters and in which:

Figure 1 is a horizontal plan of the filter assembly looking down with the upper part of the filter removed, i

Figure 2 is a vertical section or side elevation` with parts of the structure omitted for the pur` pose of clarity,

Figure 3 is a transverse vertical section or end y elevation through the lter assembly,

Figure 4 is an isometric View of the filter slurry pan arrangement,

Figure 5 is a side elevation of a filter disk,

Figure 6 is a more detailed elevation of a portion of the filter disk showing a filter sector with parts removed for clarity,

Figure 7 is a vertical section of a filter sector taken along the lines 'I-l of Figure 6,

Figure 8 is a detailed section of one end of the sector taken along the lines 8-8 of Figure 6,

Figure 9 is a detailed elevation of the deflector assembly illustrating the method of mounting the deflector on the wax trough and the cooperation of the catch pan with the wax trough,

Figure 10 is a detailed section of the deflector assembly taken along the lines Ill- IB of Figure 9,

Figure 11 is a detailed section taken along the lines II-H of Figure 9 when the sector is in pressure,Y

the drawings.

trated in the drawings.

tain of the supporting lugs I2, and these internal lugs support I beams I3 which carry bearings Irl in which shaft I5 is journaled. One end of this shaft is connected by coupling means I6 to a driving shaft I 'l journaled in sleeve bearing I8, a suitable stuffing box I9 being provided to prevent the escape of any gases from the pressure vessel. At the otherr end of this shaft we provide a master valve 2li held against suitable bearing surfaces on the shaft by a spring or other resilient means 2|. T he angular position of the master valve may be controlled by rod 22 pivotally connected to a lug 23 and extending through the casing wall through a gas tight packing to 4external control means 24. The filtrate port of the master valve is connected by flexible conduit 25 to a filtrate line connection 25. The Wash-liquid port of the master valve is connected by flexible conduit 2l to a wash-liquid line connection 28. The blow-back port of the master valve is connected by flexible conduit 29 to a blow-back line connection 3l).

Shaft I5 is provided with horizontal ducts 3| which communicate with the master valve and with the various lter disk sectors. A valve is provided in each of these ducts adjacent the master valve and any one or more of these ducts may be closed by means of a retractable wrench 3 2 which may engage valve closure means 33 and which may be retracted and externally controlled by external control means 34. Valve control means 34 is immediately behind valve control means 24 in Figure 1l as shown in Figure 3.

Figure 3 the valve control means 3d is shown to be above valve control means 24 and in line with the peep hole windows (rod 32 does not extend through the peep hole window but is back VOf it).

Electric lights 35 are provided in the pres- '.sure. vessel for illuminating the interior thereof. 'Eeel'holes 36 are spaced at intervals along the Vmoisture, on the outside glass at low temperatures and the inside glass is sprayed with propane from Y lines 38 so that clear vision may at all times be assured. These peep holes may be opposite the filter cake discharge assembly and opposite the liquid level control valve, the master valve, etc.

T o facilitate assembly and repair of the filter We may provide a trolley beam 39l along the inner top of the pressure vessel. Wheels Il@ of a travcling crane or' equivalent lifting and conveying means may run back and forth on this I beam between stops 4l (Figure 2). The filter sectors 42 are clamped on shaft` I5 by tie rods 43 and steel strap 42a, after the shaft has been mounted in bearings -I4, each filter sector leading to its corresponding duct 3 I. From 4 to 24 sectors may makeup a disk, 8 sectors being illustrated in Also any number of disks may be mounted along the shaft,v 6A disks being illus- A filter disk assembly is illustrated in Figure 5 and the detailed structure thereof Will hereinafter be more fully described. ,fllhelowel nhalfof each disk is surrounded by a slurry pan or tank 46 which is welded to channel arcanes vidual slurry pans fit rather closely around the lower half of the filter disk leaving room, of course, for the deposit of a filter cake of desired thickness. The arrangement of these slurry pans is most clearly shown in Figure 4. The upper parts of these pans are connected to each other by hemcylindrical shells 46 which surround the lower half of shaft I5. The bottoms of these tanks are connected to each other by conduits 41 and a sump V43 is provided in order that all slurry may be removed from the tanks through line 49 to draw-off line 58. A slurry is introduced into thesetanks through feed line I, manifold 52 and branch lines 53 (Figure 1) The rate at which feed slurry is introduced into the pans is regulated by valve 54 in accordance with liquid level control means 55 which is actuated by a float 56 in liquid level well 51 which communicates with one or more of the tanks 44 by openings 58. When the slurry level tends to get too high valve 54 is gradually closed and when the slurry level tends to get too low, valve 54 is gradually and automatically opened.

The use of individual and relatively small pans is an important feature of our invention because it prevents the hold-up of a large amount of slurry liquid. In the filtration of wax from propane-oil solutions it' has been found that the elimination of slurry hold-up brings about a remarkable increase in filter rates. For dewaxing as well as for other purposes it is desirable to prevent sedimentation in the slurry tanks and for this purpose we provide agitator or scraper blades 59 on the ends of tie rods 43 so that as the disk rotates in the slurry pans these agitator or scraper' blades prevent sedimentation and maintain solids in uniform suspension. Any number of such blades may be'mounted around the periphery of the disk, on the tie rods or elsewhere.

In the upper part of the pressure vessel and on both sides of the filter disks we provide liquid spray means 66 which are supplied with liquid such as propane through manifold 6| and line 62 for washing oil from a wax filter case. Any number of such sprays may be employed. Similarly we may employ sprays 63 of-kerosene or any other wash liquids, such sprays being manifolded by line 6-4 connected to line 65, for periodically washing the filter leaves. Disk sprays 66 manifolded by line 61 and supplied with liquid propane through line 58 may alsobe employed for spraying the disk at about or just prior to the point of filter cake discharge. This provides a moist cake for discharge and it provides the blow-back liquid in corrugations as will be hereinafter described.

The filter cake is discharged by the conventional blow-back through the filter leaves and is deected by deflector blades 69 into troughs I8 for removal from the system by screw conveyor 'H in conduit i2. The troughs 'I0 are between walls 44 of adjacent pans but extend downwardly for discharging filter cake to screw conveyor 'I I in conduit 12 as shown in Figure 3.

AIn order to prevent run-down wash-liquid from contaminating filter slurry we provide catch pans 13 between adjacent disks above shaft I5. This catch pan serves as a trough to deflect any rundown liquid into troughs 10.

Referring now to Figures 6, '7 and 8 we will describe in greater detail the structure of our improved lter sectors. These sectors may `be formed by pre-cast complementary side members I4 provided with registering portions or bosses 14a. The side members are held together in peripheral member 15, which forms the leading and trailing edges of the sector, held together by bolts or screws 16. The. walls of the side members are convex and a filter element 11 is sealed and held in place thereon by caulking means 18, for example by use of a rope caulking means in a suitable caulking groove in peripheral element 15. Instead of individually caulked filter elements we may of course employ filter bags or any equivalent structure but we prefer to employ the caulking arrangement in order that the leading and trailing edges of the filter sector may be more readily, adapted to serve as a guide for wire wrapping 19. The leading and trailing edges of the sector are provided with grooves 86 or with lugs or equivalent guide or spacing means and a wire is spirally wrapped around the lter element on the sector to hold the filter element in place during blow-back operations and to protect the filter element against the scraping action of the filter disk deflector blade. The convex surfaces of the filter sector and this wire wrapping constitute an outstanding feature of our invention because it prevents any appreciable fiexing of the filter element during blow-back operations; in other words, the convex surfaces make it possible for the wire to secure the filter element in a manner which would be impossible on lter sectors having fiat sides. The continuous wire wrapping is important because it has been found that individually welded wires are entirely unsatisfactory and lead to constant breakage problems. It will be noted that the wire wrapping is at substantially right angles to the radius of the filter disk so that the wires may slide freely against the cake deflector and prevent this cake deflector from scraping the filter surfaces.

The complementary side wall sector elements are designed to provide channels 6| leading to the discharge opening 82. Both sides of the sector are provided with recesses or corrugations 83 which empty into troughs 84 and channels 8| for conveying filtrate from the filter element to ducts 3l in shaft I5. An outstanding feature of our invention is the design and arrangement of these troughs or corrugations 83. The word corrugations is intended to mean a depressed area or space in which liquid may be collected. One end of these corrugations is closed by a dam 85. During the filtration and initial washing period when a filter sector is moving upwardly, these dams are above troughs 84 so that all liquid is quickly and completely drained out of the corrugations. During the latter part of the washing step and as the sector moves downwardly toward the cake discharge point in the cycle the dams are in the lower position so that each of these corrugations tends to remain full of liquid. The filter sector as shown in Figure 6 is moving in a counterclockwise direction; the filter sectors in Figure 3 are moving in a clockwise direction. When the sector reaches the blow-black point it is thus liquid instead of gas which is initially blown back through the filter element and by the means hereinabove described we may supply a relatively small amount of blow-back liquid throughout the entire area of the filter sector. Liquid blow-back is remarkably more effective than gas blow-back in obtaining a clean cake discharge, in preventing any plugging of the filter and in reconditioning the lter for reuse. After the liquid has been filterv element a considerable amount of blowl back gas passes through the lter element and the continuous introduction of this blow-back gas into the filter supplies a considerable amount of the pressuring fluid for the operation of the filter.

We have already described the Ycatch pan for preventing run-down liquid from contaminating slurry in tanks 45 but We have found that additional means must be provided to preventrundown liquids on the tie rods from contaminating the slurry in tanks 4d. We therefore mount cups 86 at such low point on each tie rod that they will collect any run-down liquid and We provide these cups with pouring spouts 8i for deflecting this run-down liquid into catch pans i3 or into receivers (not shown) for separate removal. The use of such cups on the tie rods is particularly important in those caseS,Where the filter element is Washed With kerosene or any other liquid which is desirably kept out of the slurry undergoing filtration. The catch pans 'i3 are sufficiently tapered at each end to avoid interference with cups B and these catch pans are adjustably mounted at one end to brackets 88 and at the other end to brackets 89 as is clearly shown in Figure l2. Catch pans 'I3 may discharge into a separate draw-olf line instead of into the Wax trough.

The structure of the cake defleetor and the mounting therefor are clearly shown in Figures 9 to 13 inclusive. Deflector blade 69 is secured to a floating beam Sil which is pivotally mounted at each end on pintles SI and 9| carried by Vsupport arms 52 and E2 which in turn are mounted on pivots 93 and S5. Pivot 93 is carried by the end of bolt t@ which may be set` at any desired position by means of lock nuts d5. Bolts 94 eX- tend through a bracket or lug 95 which may be Welded to a Wall of trough I or which may be adjustably secured thereto by bolts or other conventional means. Similarly, pivots 83 may be held in adjustable vertica1 position in slots Si by means of bolts S8 and the bracket S9, which carries the upturned member containing slot 9i, may be adjustably mounted on the outer edge of trough i@ by means of bolts |90, the lateral positioning being possible by virtue of slots ISI. From the structure hereinabove described it will be seen that beam 95 and deiiector E9 may be adjusted in any direction and that this beam will have freedom of motion both around pivots 93 and S3 and around pintles 9| and 9|.

Compression springs |162 and |83 urge the inner and outer ends of the beam toward the lter disks and thus hold deflector blade 69 Retractor rods |94 and |95 extend loosely through openings in outwardly extending ends of beams 90 and collars |06 are keyed on these rods on both sides of alternate beams. The ends of these retractor rods are adjustably secured to threaded collars |81 and |338 the threads in collar Il engaging left-hand threads and the threads in collar |88 engaging right-hand threads on rod Iil which extends through stuffing box |-|il .to'eXternal control means' I I By turning hand.

wheel III in one direction each of the deilector blades may be thus moved toward its corresponding filter disk and by turning the hand Wheel in the other direction each of the deector blades may be moved away from its corresponding filter disk and entirely out of contact therewith.

t Will thus be seen that We have provided means for observing the operation of the pressure filter and means for operating theV master valve 20, for controlling the opening in the filter ducts 3|, and for controlling lthe position of the filter cake defiectors BS all from points outside of the pressure casing. The supply of Wash-liquids and the control of the cake removal means is likewise outside of the pressure casing. If for any reason it should be necessary to make repairs, iiuids may be Withdrawn from the filter and access may be obtained by removing manhole cover |I. VWorkmen may enter the filter and stand on gratings I2 While making the necessary repairs. A drain line |I3 is provided for removing any liquids that may accumulate in the bottom of the pressure vessel and a gas vent |I4 may be connected to suitable pressure indicator, safety valve, and control means and may lead to any suitable blow-down tank. If desired the slurry from tanks 4d may be discharged into the filter shell through valved means I |5.

The improved lter structure and filter assembly hereinabove described is particularly adaptable for the dewaxing of numeral oils with selective solvents or with normally gaseous diluents. Such filters may be employed for example in the system described in Forrest et al. 2,143,872. The method of operating our improved lter should be apparent from the above detailed description. To summarize briefly, a slurry of crystalized Wax in liquid propane may be introduced through line 5I (Figure 3) to pans or tanks 44 in amounts controlled by valve 54 which is opened or closed in accordance with liquid level control means 56. The vaporization of propane from the slurry as Well as liquid propane used for Washing, as will be hereinafter described, builds up a pressure in the vessel which forces the liquid propane together with dissolved oil through the filter elements While leaving the Wax crystals as a lter cake on the outside of the filter element. The ltrate of liquid propane and dissolved oil flows through the passages in the filter disk and thence from the filter disk through opening 82 to a horizontal duct 3| in shaft I5 (Figure 6). Each of these horizontal ducts is provided with a separate valve indicated by valve closures 33 (Figures 1 and 2) which can be controlled from outside of the filter casing by means of retractable wrench 32 so that when visual observation through peepl'ioles 36 indicates that any particular sector is not functioning properly the flow through that sector may be stopped. The ducts 3| in shaft I5 lead to master valve 2U which is well known in the art and hence requires no further description. Such a valve, for example, is described in detail in U. S. Patent 1,659,699. The filtrate from the master valve is Withdrawn through flexible conduit 25 land discharged from the casing through line raised out of the solution is changed by the :master valve from a filtrate port to a wash duced through lines 62, 62', etc. and is distributed by lines 6| and nozzles 66 as a spray over the wax cake on the filter elements. A portion of this wash liquid vaporizes to supply the pressure in the lter for forcing the liquid through the cake and the filter element. Wash liquid which runs down the filter sectors while they are in the upper position is caught by pans 'i3 and is deected away from the slurry tanks 44 so that it will not contaminate or warm up the slurry which is undergoing filtration. Some liquid may run down tie rods 43 and in order to prevent such liquid from contaminating the slurry, cups 86 are provided which accumulate any run down liquid while in the vertical position and pour this accumulated liquid into pan 73 through spouts 81 as the cup moves downwardly during the rotation of the filter.

To facilitate filter cake discharge it is desirable that the cake be moist and 'additional propane may be introduced through line 6l for that purpose. Filter cake is discharged by conventional blow-back through the filter leaves and is defiected through chutes 'l to conduit 12* through which the wax or petrolatum is discharged. If defiectors rub on the filter element itself it may smear the crystalized wax over the filter element causing it to become clogged. During the blow-back or discharge operation there is a tendency for the filter element to be distended by the blow-back gas. To prevent appreciable distension and also to keep the filter element out of contact with the defiector it is desirable to have a wire wrapping but the use of wire Wrappings on ordinary flat sided filter sectors presented such serious lproblems that heretoforeno apparatus of this type has proved commercially satisfactory for propane dewaxing operations. By employing the convex filter element supporting surfaces and effecting the wire wrapping in the manner hereinabove described these problems were solved. 'Ihe use of convex surfaces, however, provided a new problem of defiector design because the deiiector, to be effective, must follow the contour of each sector as it passes the wax removal stage. The deflector mounting as hereinabove described permits the deflector to follow the contour of each sector during the continuous rotation of the disk.

Another feature of the invention facilitating cake discharge and cleaning of the filter medium lis the arrangement of corrugations and dams shown in Figure 6. As the filter sectors move downwardly from the Washing position to the cake discharge position, these dams retain Aliquid in the corrugations. When the filter sector is connected through the master valve with the blow-back port, this liquid is forced in a reverse direction through the filter element, this liquid blowback being remarkably effective for obtaining a clean cake discharge,

for preventing any plugging of the filter and for reconditioning the filter for reuse. After this reconditioning step the filter is again irnmersed in the slurry and the above sequence of steps is repeated. From time to time the operation of the filter may be discontinued and the filter elements may be washed with kero- 10 sene, introduced through line 55- for dissolving any deposits on the filter elements which are not soluble in propane. The invention' is not limited, however, to the use of normally gaseous liquids nor to the dewaxing of mineral oils but may be employed for any purpose where it is desired to separate lterable solids from liquids. While we have described a preferred example of our invention it should be undrstood that our invention is not limited to the structure or details of construction hereinabove described since various modifications and alternative constructions will be apparent to those skilled in the art from the above detailed description.

We claim:

1. In a continuous rotary disk filter comprising a casing, a substantially horizontalk rotatable shaft in said casing, a plurality of filter secto-rs mounted on said shaft to form a plurality of filter disks, interconnected slurry tanks for the lower part of said disks, a filter cake discharge means between adjacent slurry tanks, defiector blades for defiecting filter cake from said disks vinto said discharge means, means for mounting said deflectors for -movement toward and away from the filterl disks and also for movement in a radial plane of the filter disk and resilient means for holding each end of said defiectors against the filter disks.

2.A The apparatus of claim 1 which includes means for permitting the observation of filter cake defiectors in said filter, and means extending through said casing and controllable' outside of said casing for simultaneously moving all of said deflectors toward and away from said disks. f f

3. In a continuous rotary disk filter comprising a casing, a substantially horizontal rotatable shaft in said casing, a plurality of filter sectors mounted on said shaft to form a plurality of filter disks, each of said sectors being of convex surface and having lter elements secured thereto by meansof a wire wrapping, interconnected slurry tanks for the lower part of said disks and a filter cake discharge means between adjacent tanks, the improved structure which comprises defiectors for bearing against said wire wrapping and directingl filter cake into said discharge means, a separatev beam for supporting each of said delectors, supporting arms for said beams, means for pivotally supporting said beams on said supporting arms, brackets secured to a fixed portion of the filter structure, means for pivotally mounting said supporting arms on said brackets and means for adjusta'bly positioning said brackets whereby the deflectors may follow the wire wrapping on the convex surfaces of the filter sector on the rotation of the rotatable shaft.

Ll. The apparatus of claim 3 wherein the pivotally supported beams, pivotally mounted supporting arms and adjustable brackets are employed at both ends of each'supporting beam.

5. The apparatus of claim 3 wherein the beam extends beyond periphery of the filter disk and wherein the structure includes resilient means for holding the defiectors against the wire wrapping. I

6. The apparatus of claim 3 which includes pivotal beam mountings, pivotally mounted supporting arms, and adjustable brackets at both ends of said supporting beam, resilient means for holding the deflector against the wire wrapping and means controllable from a point outside of the casing for simultaneously moving the deflectors toward and away from said filter disk.

7. In a continuous rotary disk filter, a casing, a substantially horizontal rotatable shaft in said casing, a plurality of filter sectors carrying filter elements mounted on said shaft to form a plurality of filter disks, said shaft and filter disks forming a rotating filter structure, interconnected slurry tanks for the lower part of said disks, means for spraying a liquid against the upper part of said disks, a lter cake discharge means, a catch pan, means for adjustably mounting said catch pan in iixed position above the level of said slurry tanks, and means secured to the rotating filter structure between the filter elements and the shaft for collecting run-down liquid, said lastnamed means being provided with a spout for directing said liquid into said catch pan as the iilter structure rotates and said catch pan having a spout for deflecting said liquid away from the slurry tanks.

8. In a continuous rotary disk filter comprising a casing, a substantially' horizontal rotatable shaft in said casing, a plurality of iilter sectors carrying filter elements held on saidv shaft by tie rods to form a plurality of filter disks, interconnected slurry tanks for the lower part of said disks, means for applying a wash liquid on the upper part of said disk, a iilter cake discharge means between adjacent slurry tanks, a catch pan mounted above said shaft between adjacent disks and provided with means for deflecting run-off liquid from filter cakes to the wax cake discharge means, and collectingA cups secured to the sector tie rods between the filter elements and the shaft for collecting liquidwhich runs down said tie rods, said collecting cups being provided with pouring spouts so that the liquid therefrom is'directed into said catch pans during the rotation of the filter disks.'

9. A continuous disk filter which comprises a gas-tight casing, means for introducing a fluid into said casing for providing pressure therein, means for rotatably supporting a horizontal shaft in said casing, a horizontal shaft rotatably mounted in said supporting means, driving means outside said casing and connected to one endl of said shaft, said shaft end extending through a substantially gas-tight journal to a point outside of the casing, 'a plurality of disk sectors, filter elements on lsaid sectors, said sectors being mounted around saidshaft by tie rods to form a plurality of filter disks, a master'valve on the end of said shaft which is inside the gas-tight casing mea-nsl for conveying liquid from corresponding sectors in each disk to said master valve, conduits for conveying liquids from said master i' valve to points outside of said casing, a conduit for conveying blow-back gas from a point outside of said casing to said master valve, a slurry tank closely disposed around the lower part of each disk, communications between said slurry tanks for maintaining substantially the same liquid level in all of said tanks, means for introducing slurry into said tanks and for regulating the liquid level of slurry therein, a cake discharge trough between adjacent slurry tanks, deectors for deiiecting filter cake from adjacent sides of said disks to said trough, means for movably 12 mounting said deectors so that they may follow the contour of said disks and resilient means .for urging said deflectors against-,said disks, a catchpan mounted above said shaft between adjacent disks and discharging into said trough, cups secured to said tie rods between said filter elements land said shaft whereby run-down liquids may be collected and discharged into said catch-pan, means for spraying a wash-liquid on the upper part of said disks, means for removing filter cake from said casing and means for controlling the operation of the filter from a point outside said casing,

10. The apparatus of claim 9 which includes agitator blades mounted on the periphery of said disks for preventing sedimentation of solids in said slurry tanks. Y

11. In a continuous rotary disk filter of the type comprising a casing, a substantially horizontal rotatable shaft in said casing, a plurality of iilter sectors mounted on said shaft to form a plurality of lter disks, a separate slurry tank for the lower portion of each filter disk said tank being of sufcient width to permit a cake deposit on the disk .but being suiiiciently narrow to prevent large accumulations of filter slurry, communications between the upper parts `of said tanks in the form of a substantially hemicylindrical shell around the bottom of the shaft, conduits connecting the tanks at the bottom thereof, a draw-oli sump and a conduit leading therefrom for draining slurry from said tanks, a liquid level well communicating with at least one of said tanks, a liquid level indicating means in said well, means for controlling the amount of slurry introduced into said tanks in accordance with said liquid level indicating means, filter cake troughs between adjacent tanks, deilectors for deiiecting lter cake from said disks to said trough, mechanical means for mounting said deflectors for movement toward and away from the filter disks andalso for movement in a radial plane of the filter disk whereby they may follow the contour of the disks, resilient means for urging said defie'ctor toward said filter disks'and means for continuously removing filter cake from said casing.

12. A continuous rotary disk filter comprising a casing, a substantially horizontal rotatable shaft in said casing, a plurality of iilter' sectors mounted on said shaft to form a` plurality of filter disks, each sector having a convex outer surface, wire positioning means at its leading and trailing edges and a Vspiral wire wrapping for holding a filter element against the convex surfaces of each sector, interconnected slurry tanks for the lower part of said disks, a filter cake discharge means between adjacent slurry tanks, deiiector plates` for defiecting filter cake from said disks into said discharge means, means for mounting said deflectors for movement toward andaway from the filter disks and also for movement in a radial plane of the filter disk, and resilient means for holding said deflectors against the filter disk. Y

JOHN T. DICKINSON. ARTHUR R. MOORMAN. 

